Operational condition: Mole fraction = 0 (Liquid)
| Temperature, K - Liquid | Activity coefficient of Ethyl Acetate (2) - Liquid |
|---|---|
| 303.16 | 3.252 |
| 313.17 | 3.054 |
| 323.20 | 2.878 |
| 333.16 | 2.706 |
Operational condition: Mole fraction = 0 (Liquid)
| Temperature, K - Liquid | Activity coefficient of Ethyl Acetate (2) - Liquid |
|---|---|
| 303.16 | 3.252 |
| 313.17 | 3.054 |
| 323.20 | 2.878 |
| 333.16 | 2.706 |
Operational conditions:
| Mole fraction of Dodecane (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
|---|---|
| 0.0232 | 0.2360 |
| 0.0541 | 0.5030 |
| 0.0898 | 0.7710 |
| 0.1316 | 1.031 |
| 0.1800 | 1.279 |
| 0.2292 | 1.478 |
| 0.2790 | 1.628 |
| 0.3296 | 1.74 |
| 0.3789 | 1.817 |
| 0.4062 | 1.849 |
| 0.4261 | 1.859 |
| 0.4718 | 1.874 |
| 0.4736 | 1.868 |
| 0.5534 | 1.798 |
| 0.6470 | 1.612 |
| 0.7424 | 1.309 |
| 0.8396 | 0.8960 |
| 0.9339 | 0.4230 |
Operational conditions:
| Mole fraction of Dodecane (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
|---|---|
| 0.0232 | 0.2360 |
| 0.0541 | 0.5030 |
| 0.0898 | 0.7710 |
| 0.1316 | 1.031 |
| 0.1800 | 1.279 |
| 0.2292 | 1.478 |
| 0.2790 | 1.628 |
| 0.3296 | 1.74 |
| 0.3789 | 1.817 |
| 0.4062 | 1.849 |
| 0.4261 | 1.859 |
| 0.4718 | 1.874 |
| 0.4736 | 1.868 |
| 0.5534 | 1.798 |
| 0.6470 | 1.612 |
| 0.7424 | 1.309 |
| 0.8396 | 0.8960 |
| 0.9339 | 0.4230 |
Operational conditions:
| Mole fraction of Dodecane (1) - Liquid | Mass density, kg/m3 - Liquid |
|---|---|
| 0.0970 | 860.06 |
| 0.1460 | 846.23 |
| 0.1976 | 833.46 |
| 0.2508 | 821.88 |
| 0.2979 | 812.79 |
| 0.3903 | 797.68 |
| 0.4943 | 783.92 |
| 0.6000 | 772.56 |
| 0.6909 | 764.45 |
| 0.7392 | 760.65 |
| 0.7931 | 756.85 |
| 0.8213 | 754.91 |
| 0.8798 | 751.38 |
| 0.9374 | 748.08 |
Operational conditions:
| Mole fraction of Dodecane (1) - Liquid | Mass density, kg/m3 - Liquid |
|---|---|
| 0.0970 | 860.06 |
| 0.1460 | 846.23 |
| 0.1976 | 833.46 |
| 0.2508 | 821.88 |
| 0.2979 | 812.79 |
| 0.3903 | 797.68 |
| 0.4943 | 783.92 |
| 0.6000 | 772.56 |
| 0.6909 | 764.45 |
| 0.7392 | 760.65 |
| 0.7931 | 756.85 |
| 0.8213 | 754.91 |
| 0.8798 | 751.38 |
| 0.9374 | 748.08 |